[0001] The present invention relatec to an elastic aultilayer film, and mere particularly
to a two-layer film suitable for use in the packsging of poultry.
[0002] Generally, one of the typical commtrcial packeging operations of frozen poultry includes
the following steps:
1. Enclosing boneless turkey meat in a string betting;
2. Enclosirg the netted turkey meat in an elastic bag by mechanically expanding the
bag to aaproxi- mately 140% of its normal circumference, placing the netted turkey
meat in the bag, and thereafter, sllowing the bag to relax to its normal size to form
a tight package;
3. Generally evacuating the air from the bag and clipping the end of the bag closed;
4. Quick freezing the bagged turkey meat to a temperature as low as about -40° C;
and
5. Shipping the frozen turkey meat in the bag.
[0003] A bag suitable for these steps must be formed from a film exhibiting good dimensional
stability, praduction controllable thickness, non-tacky surfaces, and economical production.
In addition, the film mist have good resictance to abrasion and impact because the
shipping of the bagged turkey meat usually results in the abrasion of bags sgainst
each other as well as their mutual impacts.
[0004] One prior art file used to fabricate bags for the turkey meat is a plasticized vinyl
film. The bags formed from this film have the dravback that an unsaticfactory percentage
of bags became damaged during the shipping step.
[0005] In accprdaoce with the present invention, there is provided an elastic multilayer
film suitable far use in connection with the packaging of poultry, comprising a first
outer layer including a plasticired polyvinyl chloride having an inherent viscosity
greater than about 1.10 and having a plasticizer content of from about 35 phr to about
40 phr, and a second outer layer including an ethylene vinyl acetate copolymer having
a vinyl acetate content of from about 16% to about 20% by veight and beving a melt
flow of from about 1.0 to about 3.0 decigrams per minute. Preferably, the first outer
layer has a thickness of from about 1.75 mils to about 2·0 mils and the second outer
layer has a thickness of from about 0.5 mil to about 0.75 mil.
[0006] Praferably, the film consiats of the two outer layers. In addition, a thickness of
0.75 mil for the second outer layer and vinyl acetate content of about 18% by veight
are preferable.
[0007] Preferably, the plasticizer is at least 27 phr of a food approved plasticirer such
as dibutyl sebacate or a di-n-hexyl azelate which are low temperature plasticirers.
The remainingplisticizer is preferably an epoxidized soybean oil.
[0008] An ethylene vinyl acetate copolymer having a vinyl acetate content greater than about
20% by weight generally results in a film having insufficient strength. For a vinyl
acetate content less than about 16% by weight, there is poor adhesion between the
two outer layers.
[0009] An ethylene vinyl acetate copolymer having a selt flow less than about 1.0 decigram
per minute is undesirable because of the difficulty in processing this type of resin
at die temperatures preferable for plasticized pclyvinyl chloride extrusion. A melt
flow too high tends to weaken the puncture resistance of the film.
[0010] Generally, the processes of forming the film of the invention and bags can be carried
but using conventional blown film extrusion processes.
[0011] Preferably, a two-layer film is coextruded into tubular form, air cooled to a temperature
below the softening point, and then wound into rolls for subsequent iabrication into
bags. It has been discovered that the temperatures of the elbow end die of the extrusion
device are critical for obtaining satisfactory films according to the invection and
these temperatures must be adjusted so that the temperature of the inside of the extruded
tube of file and the temperature between the two layers is relatively cool. These
temperatures are readily identifiable tc persons in the art because the film leaving
the extrusion device has a visual appearance of having a low gloss level. The preferred
conditions correspond to a temperature of about 425" F at the exit of the die.
[0012] Illustrative, non-limiting examples of the practice of the invention are set out
below. Fumerous other examples can readily be evolved in the light of the guiding
principles and teachings contained herein. The examples given herein are intended
mainly to illustrate the invention and not in any sense to linte the manner in which
the invention can be practiced.
[0013] All percentages and parts stated herein are by weight unless otherwise stated.
[0014] As used berein, the term "phr" has the conventional meaning of parts per 100 parts
of polymer.
[0015] The materials described herein have their properties determined in scordapce with
the following test methods:
Melt Flow - ASTM D-1238 -57T at 44 psi and 190°C
Viscosity - ASTH D-1243
[0016] In the examples, the meterials shown in Trbles 1 and 2 were employed:

Examples 1 to 9
[0017] Two layer films were produced with a first outside layer of a plasticized polyvinyl
chloride including 27.5 phr of dibutyl sebscate and 10.0 phr of epoxidized soybean
oil, and a second outer layer of an ethylene vinyl acetate co- polymer as shown in
Table 3.
[0018] Generally, the extrusion equipment includes a 2-1/2 inch 16:1 L/D HRM oil bsated
extruder to feed the plesticized polyvinyl chloride. The barrel temperature was

maintained at about 300° F and the screw speed was about 22 rpm. The ethylene vinyl
acetate extruder was a 1-1/4 inch - 18:1 L/D TEC extruder with the barrel teaperature
maintained at about 320° F and a screw apeed of about 34 rpm. A 60 mm diameter two
layer die was used with the plasticized vinyl chloride as the inner layer and the
ethylene vinyl acetate capolymer as the outer layer. The die base temperatures were
maintained at about 425° F while the exit temperature veried from about 425° F to
about 475° F. Conventional blown film methods were used to cool and flatten the bubble.
The film speed was about 50 fpm.
[0019] For the examples 1 to 9, the EVA's A, B, C, D, and E were used as well as different
layer thicknesses. Observätions on the extrusion performance and layer adhesion are
indicated in addition to varions physical properties of the films. The TITE-WRAP test
is a test especially relevant to the intended use of the film of the invention. The
tubular film is cut to a length of about one foot long and powdered to reduce its
coefficient of friction and placed on two sets of jews which are connected to pneumatic
cylinders. The jaws are rapidly opened to that the circumference of the film is increased
by about 50%.
[0020] Although EVA's C and D showed acceptable results for the respective examples 5 and
7, the unsatisfactory results of the related examples 6 end 8 indicate that the layer
thicknesses suitable for conmercial use night be unreliable. The EVA E presented problems
in the extrusion because of the high viscosity, as indicated by the relatively low
melt flow, is untatisfactory at the temperatures tuitable for vinyl extrusion.
[0021] The EVA's A and B showed satisfactory performince in the propertice tested. Surprisingly,
a film hiving a second outer layer about 0.5 mil in thickness was stronger then a
film having a second outer layer about 1.0 mil in tnickness.
Examples 10 to 17
[0022] Examples 10 to 17 were carried out with an endeavor to produce a film using conventional
methods in order to compare the perfortance of additional polymers for the second
outer laper. The first outer layer was the same as the example 1.
[0023] Table 4 shows the results of the examples 10 to 17. None of these examples produced
a film satisfactory for commercially packaging poultry.
[0025] Examples 18 to 21 were carried out to demonstrate the necessity of maintaining the
extrusion conditions relatively cool.
[0026] The example 18 is a known single layer plesticired vinyl used for packaging poultry.
The examples 19 to 21 are films of the inventions with the dimensions shown and comprising
the materials of the example 1. Also shown in the Table 5 are the extrusion conditions
for the films and the breakage during packaging and shipping of bags fabricated from
the films.
[0027] The Table 5 shows the superior performance of the film according to the invention
and the importance of the extrusion temperature on bag performance.
Examples 22 to 40
[0028] Examples 22 is a conventional single layer film of plasticized vinyl and examples
23 to 40 are films with the materiels of the example 1 prepared under various conditions
and different layer thicknesses as shown in Table 6.
[0029] Generally, the temperatures of the inside of the tubular film and between the layers
can be estimeted by a person having prdinary skill in the art by visual appearance
(glase) on the film. Temperatures at the exit of the die which are broadly referred
to as "cold", "warm", and "not" correspond respectively to about 425°F, about 450°
F, and about 475° F.
[0030] The single layer film of the example 22 was included to provide a comparison to the
prior art.
[0031] The Dynamic Tensile test includes cycling a sample to a 50 inches per minute jaw
speed from 0 to 200% elongation at about -40° F and recording the average number of
cycles to failure.
[0032] The film condition was visually determined based on the gloss of the film.

[0033] The plasticized polyvinyl chloride in the examples 23 to 38 was the same as in the
previous examples. In the examples 39 and 40, the plasticizer was 30 phr dibutyl sebacate.
[0034] The examples 24 to 28 show that reducing the temperature of the extrusion system
pravides an improved tensile strength.
[0035] The examples 29 to 35 generally were run at relatively cool extrusion temperatures
and provide a comparison between films having layers of different thicknesses. While
the impact strength of each of the examples 32 and 33 was high, the dynamic tensile
strength for each was low.
[0036] For the examples 36 to 40, the thickness of the first puter layer was varied slong
with the smount of plasticizer. These examples provided the best results for both
the dynamic tensile and the impact strength tests.
[0037] We wish it understood that we do not desire to be limited to the exact details shown
and described, for obvious modifications will occur to a person skilled in the art.
1. An elastic multilayer film suitable for use in connection vith the packaging of
poultry, comprising a first outer layer including a plasticized polyvinyl chloride
having an inherent viscosity greater than about 1.10 and having a plasticizer content
of from about 35 phr to sbout 40 phr; and a second outer layer including an ethyleae
vinyl acetate copolymer having a vinyl acetate content of from about 16% to about
20% by weight and having a melt flow of from about 1.0 to about 3.0 decigrams per
minute.
2. A film as claimed in clxim 1, wherein said first outer layer has a thickness of
from about 1.75 mils to about 2.0 mils and said second outer layer has a thickness
of from about 0.5 mil to about 0.75 mil.
3. A film as claimed in claim 1 or 2, wherein the vinyl acetate is about 18% by weight.
4. A film as claimed in any one of the preceding claims, wherein said layers are in
physical contact with each other.
5. A film as claimed in any one of the . preceding claims, wherein said second outer
layer has a thickness of about 0.75 mil.
6. A film as claimed in any one of the preceding claims, wherein said plasticizer
is at least about 27 phr.
7. A film as claimed in any one of the preceding claims, wherein said plasticizer
includes dibutyl sebacate.
8. A film as claimed in any one of claims 1 to 6, wherein said plasticizer includes
di-n-hexyl azelate.
9. A film as claimed in claim 7 or 8, wherein any additional amount of said plasticizer
includes epoxidized soybean oil.
10. A film as claimed in any one of the preceding claims, wherein said melt flow is
about 1.0 decigram per minute.
11. A bag fabricated from a film as claimed in any one of the preceding claims.